Performance of cathode-supported SOFC with Ni0.5Cu0.5-CGO anode operated in humidified hydrogen and in low-concentration dry methane

被引:9
作者
Chen, Gang [1 ]
Guan, Guoqing [2 ]
Kasai, Yutaka [3 ]
You, Hong-Xin [4 ]
Abudula, Abuliti [1 ,2 ]
机构
[1] Hirosaki Univ, Grad Sch Sci & Technol, Hirosaki, Aomori 0368560, Japan
[2] Hirosaki Univ, NJRISE, Aomori 0300813, Japan
[3] Aomori Prefectural Ind Technol Res Ctr, Ind Res Inst, Aomori 0300113, Japan
[4] Dalian Univ Technol, Chem Engn Coll, Dalian 116024, Peoples R China
关键词
Solid oxide fuel cell; Cathode-supported; Bimetallic anode; Methane; OXIDE FUEL-CELLS; DIRECT OXIDATION; DEGRADATION; HYDROCARBONS; ELECTROLYTE; FABRICATION; CONVERSION; LAYER; FILM; SDC;
D O I
10.1007/s10008-011-1615-1
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
A Ni0.5Cu0.5-CGO (Ce0.8Gd0.2O1.9) anode in a LSM ((La0.75Sr0.25)(0.95)MnO3-delta )-CGO cathode-supported SOFC is tested in humidified H-2 (3% H2O) and in low concentration of dry methane, respectively. After co-sintering at 1,300 A degrees C, it was found that the A-site-deficient LSM effectively hindered the formation of La2Zr2O7 or SrZrO3. The OCVs of the cell are as high as 1.132, 1.14, and 1.147 V in humidified H-2 and 1.314, 1.269, and 1.2 V in 14.8% of dry methane at 850, 800 and 750 A degrees C, respectively, indicating that the ScSZ electrolyte film prepared by the present method is dense enough. The corresponding peak power densities are 0.396, 0.287, and 0.19 W cm(-2) in humidified H-2 and 0.249, 0.164, and 0.096 W cm(-2) in 14.8% of dry methane at 850, 800, and 750 A degrees C, respectively. The prepared cathode-supported SOFC with NiCu-CGO bimetallic anode shows long-term stability when dry methane is used as fuel.
引用
收藏
页码:2071 / 2077
页数:7
相关论文
共 34 条
[1]   Advanced anodes for high-temperature fuel cells [J].
Atkinson, A ;
Barnett, S ;
Gorte, RJ ;
Irvine, JTS ;
Mcevoy, AJ ;
Mogensen, M ;
Singhal, SC ;
Vohs, J .
NATURE MATERIALS, 2004, 3 (01) :17-27
[2]   Characterization of planer cathode-supported SOFC prepared by a dual dry pressing method [J].
Chen, Gang ;
You, Hong-Xin ;
Kasai, Yutaka ;
Sato, Hiroyuki ;
Abudula, Abuliti .
JOURNAL OF ALLOYS AND COMPOUNDS, 2011, 509 (16) :5159-5162
[3]   High performance cathode-supported SOFC with perovskite anode operating in weakly humidified hydrogen and methane [J].
Chen, X. J. ;
Liu, Q. L. ;
Chan, S. H. ;
Brandon, N. P. ;
Khor, Khiam Aik .
ELECTROCHEMISTRY COMMUNICATIONS, 2007, 9 (04) :767-772
[4]   Chemical degradation of La1-xSrMnO3/Y2O3-stabilized ZrO2 composite cathodes in the presence of current collector pastes [J].
Chervin, C ;
Glass, RS ;
Kauzlarich, SM .
SOLID STATE IONICS, 2005, 176 (1-2) :17-23
[5]   Characterisation of Ni-YSZ-Cermets with respect to redox stabilityx [J].
Ettler, M. ;
Blass, G. ;
Menzler, N. H. .
FUEL CELLS, 2007, 7 (05) :349-355
[6]  
Gorte RJ, 2000, ADV MATER, V12, P1465, DOI 10.1002/1521-4095(200010)12:19<1465::AID-ADMA1465>3.0.CO
[7]  
2-9
[8]   Degradation of the electrical conductivity in stabilised zirconia system Part II:: Scandia-stabilised zirconia [J].
Haering, C ;
Roosen, A ;
Schichl, H ;
Schnöller, M .
SOLID STATE IONICS, 2005, 176 (3-4) :261-268
[9]   Methane reforming kinetics within a Ni-YSZ SOFC anode support [J].
Hecht, ES ;
Gupta, GK ;
Zhu, HY ;
Dean, AM ;
Kee, RJ ;
Maier, L ;
Deutschmann, O .
APPLIED CATALYSIS A-GENERAL, 2005, 295 (01) :40-51
[10]   Evaluation of the cost performance of the SOFC cell in the market [J].
Ippommatsu, M ;
Sasaki, H ;
Otoshi, S .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1996, 21 (02) :129-135